EP2803478B1 - Feuille à plusieurs couches en plastique - Google Patents

Feuille à plusieurs couches en plastique Download PDF

Info

Publication number
EP2803478B1
EP2803478B1 EP14183261.8A EP14183261A EP2803478B1 EP 2803478 B1 EP2803478 B1 EP 2803478B1 EP 14183261 A EP14183261 A EP 14183261A EP 2803478 B1 EP2803478 B1 EP 2803478B1
Authority
EP
European Patent Office
Prior art keywords
outer layer
layer
multilayer film
plastic multilayer
film
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
EP14183261.8A
Other languages
German (de)
English (en)
Other versions
EP2803478A3 (fr
EP2803478A2 (fr
Inventor
Matthias Perick
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nitto Advanced Film Gronau GmbH
Original Assignee
Mondi Consumer Packaging Technologies GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mondi Consumer Packaging Technologies GmbH filed Critical Mondi Consumer Packaging Technologies GmbH
Priority to HUE14183261A priority Critical patent/HUE030040T2/en
Priority to EP14183261.8A priority patent/EP2803478B1/fr
Priority to ES14183261.8T priority patent/ES2586155T3/es
Priority to PL14183261T priority patent/PL2803478T3/pl
Publication of EP2803478A2 publication Critical patent/EP2803478A2/fr
Publication of EP2803478A3 publication Critical patent/EP2803478A3/fr
Priority to US14/809,738 priority patent/US20160059514A1/en
Application granted granted Critical
Publication of EP2803478B1 publication Critical patent/EP2803478B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/18—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
    • B32B5/20—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material foamed in situ
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B5/00—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts
    • B32B5/18—Layered products characterised by the non- homogeneity or physical structure, i.e. comprising a fibrous, filamentary, particulate or foam layer; Layered products characterised by having a layer differing constitutionally or physically in different parts characterised by features of a layer of foamed material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/065—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of foam
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/32—Layered products comprising a layer of synthetic resin comprising polyolefins
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2266/00—Composition of foam
    • B32B2266/02—Organic
    • B32B2266/0214—Materials belonging to B32B27/00
    • B32B2266/025—Polyolefin
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2307/00—Properties of the layers or laminate
    • B32B2307/40—Properties of the layers or laminate having particular optical properties
    • B32B2307/408—Matt, dull surface
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2323/00—Polyalkenes
    • B32B2323/04—Polyethylene
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2323/00—Polyalkenes
    • B32B2323/10—Polypropylene
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B2553/00—Packaging equipment or accessories not otherwise provided for

Definitions

  • the invention relates to the technical field of plastic multilayer films with at least one foamed film layer.
  • the invention specifically relates to a plastic multilayer film having a thickness between 20 microns and 250 microns comprising a foamed core layer, a first non-foamed, preferably heat-sealable outer layer and a second unfoamed outer layer having a thickness of less than 70 microns.
  • the plastic multilayer film can be provided in the context of the invention for various applications, wherein the second unfoamed outer layer should be visible to a user.
  • a typical application for the plastic multilayer film according to the invention is the production of packaging, wherein the second outer layer is visibly arranged on the outside of the packaging and the first unfoamed outer layer on the inside. If the first unfoamed outer layer is then heat sealable according to a preferred embodiment, a package can be particularly easily formed by heat sealing, either forming a film blank or continuous web by folding into a package or at least joining two film blanks or two film webs through sealing seams.
  • the plastic multilayer film has special specific advantages due to the foamed core layer, so that the plastic multilayer film is also suitable as a surface protection film, for the formation of adhesive tapes or as a kind of paper substitute.
  • the plastic multilayer film can be used both in a so-called FFS (Form Fill and Seal) method in which a bag-shaped package is formed directly in the packaging of the filling material, as well as in the production of prefabricated Packaging, which is then filled later.
  • FFS Form Fill and Seal
  • plastic multilayer film can be used for example as a cover sheet.
  • the foaming of a film layer can be done for various reasons.
  • foaming results in a lower basis weight relative to the resulting thickness of the film and thus a saving of material.
  • the mechanical properties are also improved by the greater thickness.
  • a foamed core layer is combined with unfoamed cover layers, there is a kind of plywood effect which can less easily be deformed against each other by the increase in volume of the core layer compared to a non-foamed embodiment further apart outer layers.
  • by foaming at least a film layer also affects the other physical properties of the resulting coextruded film.
  • a foamed film layer is used as a mechanical buffer in order to increase the puncture resistance or to compensate to a certain degree for mechanical deformation through the product.
  • At least one foamed film layer can also be used for thermal insulation.
  • Appropriate approaches are out JP 2001-130586 A . US Pat. No. 6,913,389 B2 . KR 2004-0005806 and KR 2004-0007381 known.
  • a foamed film layer in a film can also cause weakening which promotes tearing in a desired manner. Due to the lower density and the free spaces within the at least one foamed film layer, it can be torn relatively easily in its thickness direction. Depending on the specific embodiment, the foaming can also facilitate the layer separation with respect to an adjacent film layer, these properties can be used for the production of tear-open packaging. Moreover, even when the film tears perpendicularly to its thickness, in particular in the case of crack propagation along the production direction, weakening due to foaming ensues.
  • a pronounced anisotropy can also be attributed, depending on the production process, to the fact that the pores or cavities formed during foaming are aligned in one production direction so that tearing can be particularly easy along the longitudinal direction of these cavities or pores (ie along the production direction).
  • the use of foamed film layers for setting defined Tearing properties is for example in GB 2 110 215 B . US 4,762,230 . U.S. 4,781,294 . EP 673 756 A1 . JP 3823967 and DE 20 2005 002 615 U1 described.
  • the foaming of at least one film layer also leads to increased roughness or waviness of the film surface, this effect according to DE 2 038 557 A1 .
  • JP 2001- 055242 A and EP 1 237 751 B1 B1 is used as an advantage.
  • the ripple or roughness of the surface resulting from the foaming is in many cases also undesirable if, for example, in packaging a surface which is as uniform as possible, smooth and has a high-quality appearance is desired.
  • Another effect of a foamed film layer is known from practice that the corresponding film has a higher haze and opacity.
  • the use of color particles can also be reduced by providing a non-transparent or translucent film by foaming.
  • the increase in opacity and the use of this effect are in the EP 83 167 B1 described.
  • foaming can be carried out in particular by a chemical reaction or a physical process.
  • substances contained in the polymer melt during extrusion may volatilize or react to form a gas.
  • a blowing agent is added in the extruder to the molten plastic mass under high pressure.
  • propellants for example, water, nitrogen or carbon dioxide are suitable.
  • the foamed layer has a particularly fine-cell foam structure, which can be formed, for example, by the so-called MuCell process.
  • Devices for carrying out the process or retrofitting conventional extruders are sold by Drexel Inc., USA.
  • the MuCell method is used in particular in US 5,866,053 . US 6 051 174 . EP 923 443 B1 . EP 1 275 485 . EP 377 650 A1 . EP 580 777 B1 . US 6,231,942 . EP 996 536 A2 .
  • EP 1 040 158 B2 EP 1 131 387 B1 .
  • EP 1 539 868 B1 EP 1 337 387 A1 and EP 1 575 763 B1 described. More particularly, the present invention relates to polyethylene coextruded films in which the foamed core layer is formed according to the described MuCell method.
  • a blowing agent is added to the melt for the core layer to be foamed, which causes foaming during the extrusion or immediately after it leaves the extrusion gap.
  • the previously added under pressure of the melt blowing agent undergoes a sudden relaxation at the exit from the nozzle gap of the coextrusion.
  • the propellant is usually present within the extruder as a supercritical fluid, which combines the incompressibility of a liquid and the solution properties of a gas.
  • the blowing agent goes into solution in the polymer melt and forms there distributed a single-phase system with the plastic melt.
  • the gas dissolves out of the melt, leaving a very fine, even Foam structure is formed.
  • Particles in the core layer can favor the formation of especially many small nucleation nuclei.
  • the particles do not serve, or at least not exclusively as a favorable volume material, but are also used as a functional constituent for improving the film properties, namely for the formation of particularly many and small cavities or cells. Nevertheless, the particles can also be referred to as nucleating agents.
  • KR 2013-0100597 A and WO 2013/179947 A1 relate to other films or other plastic articles with a foamed layer or their preparation.
  • the present invention concretely relates to a plastic multilayer film having a thickness between 20 ⁇ m and 250 ⁇ m comprising a foamed core layer, a first unfoamed, preferably heat-sealable outer layer and a second unfoamed outer layer having a thickness of less than 70 ⁇ m.
  • the plastic multilayer film or at least a part of the layers of the plastic multilayer film can in particular be manufactured using the MuCell method described above, wherein blown film extrusion is preferred for simple, cost-efficient production.
  • the person skilled in various measures are known to reduce the unevenness of the second unfoamed outer layer.
  • the unevenness caused by the underlying core layer can be somewhat equalized, but then the manufacturing cost and the basis weight of the plastic multilayer film disadvantageously increase.
  • the still molten film can be introduced into a nip between two rolls or between a roll and a smoothing belt for smoothing.
  • the smoothing belt can enclose the associated roller over a larger angular range, so that the film guided therebetween is supported over a correspondingly large area, in which case a smooth surface can be achieved when the two outer layers solidify in the gap.
  • a smooth surface can be achieved when the two outer layers solidify in the gap.
  • the present invention has for its object to provide a plastic multilayer film, which is easy to manufacture and is characterized by a uniform appearance.
  • the object of the invention and the solution of the problem is a plastic multilayer film according to claim 1.
  • the second outer layer has a matte surface with a reflectometer according to DIN 67530 at a measuring angle of 85 ° of less than 40.
  • the reflectometer value thus determined is less than 30, and more preferably between 10 and 25.
  • the present invention is based in this context on the finding that the waviness still present on the second outer layer in the plastic multilayer film according to the invention is surprisingly no longer visible to a user due to the structure of the foamed core layer arranged underneath, if the plastic multilayer film adjoins the second outer layer is very dull. Even though these measures do not reduce the actual unevenness at all or at least do not significantly reduce it, the waviness is no longer visible due to the diffuse refraction of light. Astonishingly, this applies precisely to the structure resulting from foaming, which gives the user the impression of uneven waves or dents in the case of a glossy surface.
  • the reflectometer value is usually used for a comparison at a measurement angle of 85 °, although the matte properties are also evident in the measurement angles of 60 ° and 20 ° proposed according to DIN 67530.
  • the reflectometer value of the plastic multilayer film according to the invention according to DIN 67530 at a measuring angle of 60 ° is usually less than 30, preferably less than 20 and in particular between 5 and 15.
  • the reflectometer value is usually less than 10, preferably less as 5 and in particular between 1 and 3.
  • the foamed core layer together with the first unfoamed outer layer and the second unfoamed outer layer are completely coextruded, in which case a corresponding matt plastic material for the second outer layer must be provided already in this coextrusion process.
  • the plastic multilayer film thus formed can be subsequently printed only on its two outer layers. Since the plastic multilayer film alone is at least opaque due to the foaming of the core layer independently of the addition of color particles, such an imprint is preferably carried out on the second outer layer. At least if the imprint extends over larger areas, a matt ink should be used, because otherwise the existing wave structure is visible to the user again at the printed areas.
  • the second outer layer can also be provided with a coating, for example a thin matt lacquer, in order to achieve the reflectometer value according to the invention.
  • the plastic multilayer film is formed by a Kaschierverbund, on the one hand a film comprising the core layer and on the other hand, a film comprising the second outer layer, preferably by adhesive, laminated.
  • the core layer with the first outer layer and opposite the first outer layer is co-extruded with an intermediate layer, wherein the coextrusion film thus formed is laminated to the intermediate layer with a cover film which comprises at least the second outer layer.
  • the cover film can also be designed as a monofilm so that it exclusively comprises the second outer layer.
  • the plastic multilayer film is formed as Kaschierverbund, can be done in a particularly advantageous manner, an internal imprint, so that it is then optimally protected. Since this imprint is then also arranged under the hard surface of the second outer layer, there are no special requirements with regard to the quality and abrasion resistance of such an ink.
  • Orientation in the film production means stretching the film after the polymer has cooled, thereby aligning the polymer chains. Since the plastic is no longer molten in the orientation, the chains can no longer realign after stretching and remain in an elongated state corresponding to the elongation ratio.
  • the second outer layer may contain as main component preferably polypropylene (PP) or polyester, in particular polyethylene terephthalate (PET).
  • PP polypropylene
  • PET polyethylene terephthalate
  • the second outer layer thus contains at least 50% by weight of PP or PET.
  • the second outer layer may consist entirely of polypropylene or polyethylene terephthalate, with the exception of customary fillers and additives, processing aids or the like.
  • the materials mentioned are suitable both for coextrusion with the foamed core layer and the first outer layer and for the formation of a separate cover film.
  • biaxial orientation is particularly preferred for improving mechanical and optical properties.
  • the second outer layer preferably has an average waviness W a in accordance with DIN EN ISO 4287 of more than 2 ⁇ m, in particular more than 4 ⁇ m.
  • the average waviness W a is the arithmetic mean of the profile coordinate after the short-wave component (the roughness) has been calculated out by a corresponding filter on a cross section through the surface profile. Accordingly, according to the specified average waviness, the surface of the second outer layer is uneven to a considerable extent, wherein this unevenness is not visible through the mat embodiment according to the invention.
  • the cross-sectional structure differs to some extent in the direction of production and in the transverse direction, because the cavities formed by foaming or pores of the core layer are usually elongated in the direction of production.
  • the unevenness can therefore be assigned a greater wavelength in a section along the production direction than in the transverse direction, so that a glossy surface on the second outer layer can also result in a user-visible disturbing strip structure. Even such existing strip-like structures are no longer visible due to the present invention matte design.
  • the distance between a trough and an adjacent wave tip of a cross-sectional profile between 0.1 mm and 5 mm the height difference between wave trough and wave tip typically between 4 ⁇ m and 20 microns.
  • the second outer layer can be made thin, because it optically conceals the wavy structure by the matt configuration and should not compensate as a kind of buffer with variable thickness.
  • the thickness of the second unfoamed outer layer is preferably between 15 and 40 ⁇ m.
  • the core layer and the first outer layer may in particular be formed on the basis of polyethylene as the main component.
  • the coextrusion film is preferably designed in three layers, in which case the foamed core layer is arranged between the first outer layer and an intermediate layer in the coextrusion film, wherein the intermediate layer forms a surface with respect to the coextrusion film alone the cover sheet with the second outer layer is subsequently arranged. It has been found that in such a three-layer structure of the coextrusion film by suitable measures, the ripple still relatively can be kept low, so that then result in connection with the matte design of the second outer layer particularly advantageous optical properties.
  • the polymer layer comprises a polyethylene or a mixture based on polyethylene, which has a melt flow rate (MFR) according to DIN EN ISO 1133 of more than 5 g / 10 min at 190 ° C and 2.16 kg.
  • MFR melt flow rate
  • the melt mass flow rate is used to characterize the flow behavior of a thermoplastic under given pressure and temperature conditions.
  • the melt mass flow rate is often used as a comparative figure to characterize the flow properties of various plastics. It is defined according to DIN ISO EN 1133 as the mass of plastic, which flows through a capillary fixed dimension in 10 min at a given temperature and pressure.
  • the viscosity of a thermoplastic increases with the chain length of the polymers as well as with the degree of branching, which correspondingly decreases the melt mass flow rate.
  • the core layer can be formed, in particular, from particles and the polymer component based on polyethylene and optionally further processing aids, usually with a proportion of less than 10% by weight.
  • the entire polymer component based on polyethylene has a melt mass flow rate (MFR) of more than 6 g / 10 min at 190 ° C. and 2.16 kg and is therefore comparatively thin.
  • MFR melt mass flow rate
  • particles can be very uniform in the core layer at the specified melt mass flow rate in the production after exiting the gap of a coextrusion distributed form small cavities, wherein during the extrusion process after exiting the extrusion die relatively low-viscosity core layer between the first outer layer and the intermediate layer is arranged, whereby the inclusion of the core layer takes place to the outside.
  • the first outer layer and the intermediate layer have a low waviness and roughness on the surfaces of the outer layers in comparison to known polyethylene coextrusion films with a foamed core layer.
  • the melt mass flow rate the entire polymer component of the core layer is to be used.
  • the melt mass flow rate for the corresponding polymer blend must be determined.
  • the proportion of the particles in the core layer is usually between 5 and 50 wt .-%, preferably between 10 and 30 wt .-%.
  • the first outer layer and the intermediate layer serve in the coextrusion and in the foaming of the core layer as a kind of boundary, which also build up a certain back pressure with regard to the expansion of the core layer.
  • the first outer layer and the intermediate layer have a significantly higher viscosity and thus a significantly lower melt mass flow rate according to DIN ISO EN 1133 at 190 ° C and 2.16 kg.
  • the melt mass flow rate (MFR) of the two polymer components is preferably below 2 g / 10 min, more preferably below 1 g / 10 min.
  • the ratio of the melt mass flow rate of the polymer component of the core layer to the melt mass flow rate of the polymer components of the first outer layer or of the intermediate layer is at least 2.5, preferably at least 3 and particularly preferably at least 6. It is also readily possible within the scope of the invention Ratios of more than 10 can be achieved. The ratio formed in this way makes it clear that the first outer layer and the intermediate layer are significantly more viscous than the core layer. Taking these requirements into consideration, films with a relatively uniform, flat surface could be formed in the course of orienting tests.
  • first outer layer and the intermediate layer with a low melt mass flow rate immediately upon extrusion cause an increased counterpressure in the expansion of the core layer
  • the comparatively viscous layers through the formation of individual cavities and bubbles in the core layer can be less deformed.
  • the first outer layer and the intermediate layer are thus too viscous to be able to be greatly deformed starting from a substantially planar orientation.
  • the first heat-sealable outer layer and the intermediate layer may comprise polymer blends having a same or approximately equal melt mass flow rate to effect approximately the same counterpressure in the expansion of the core layer as previously described.
  • the first, heat-sealable outer layer has a higher melt mass flow rate than the intermediate layer.
  • the first outer layer provided as the sealing layer is often arranged on the inside, so that a certain slight waviness can be tolerated there, while the usually outer intermediate layer should be as smooth as possible.
  • the first outer layer may, for example, have a melt mass flow rate of 2 to 3 g / 10 min, while the intermediate layer has a melt mass flow rate of 1 g / 10 min. With such an asymmetric adjustment of the melt mass flow rate, the surface of the intermediate layer can ultimately be made even smoother, since the individual cells spread more strongly in the direction of the first outer layer during the foaming of the core layer and rather lead to unevennesses there.
  • the MuCell method described in the introduction is preferably used for foaming the core layer, wherein a microcell structure is produced in the core layer.
  • the microcell structure is characterized by a pore structure having an average pore size of less than 100 .mu.m, wherein the pore size can also be in the range between 0.1 .mu.m and 10 .mu.m.
  • the volume of the closed cavities of the core layer is a suitable characteristic feature, the volume preferably less than 50000 .mu.m 3 , preferably less than 20,000 .mu.m 3 and for example, less than 5000 microns 3 .
  • the core layer has correspondingly closed, nitrogen-filled cavities.
  • the degree of foaming can be adjusted by the amount of the blowing agent added, the viscosity of the polymer components of the core layer and the other layers, and the extrusion conditions.
  • the core layer has a density between 0.2 g / cm 3 and 0.8 g / cm 3 .
  • the increase in thickness of the core layer compared to a non-foamed layer having the same amount of polymer is thus typically between about 20% and 500%, more preferably between about 40% and 200%, most preferably between 50% and 120%.
  • the plastic multilayer film according to the invention is distinguished from a completely unfoamed film by a low weight per unit area and thus by a lower use of material, wherein adequate mechanical properties with regard to stiffness and tear strength can be achieved by suitable matching of the layer thicknesses.
  • the thickness of the foamed core layer is between 20% and 70% of the total thickness of the entire plastic multilayer film.
  • the two outer layers each have a thickness which is between about 15% and 30% of the total thickness of the polyethylene coextrusion film.
  • the polymer component of the core layer may contain as a main component a linear polyethylene, including metallocene catalyst derived types. Suitable are linear polyethylenes of high (LHDPE), medium (LMDPE) and low (LLDPE) densities. In principle, all known linear types of polyethylenes, ie alpha-olefin copolymers on the basis of polyethylene into consideration. Preferred are copolymers with hexene (C6) and octene (C8).
  • linear low density polyethylene is often advantageous to avoid overly rigid and brittle packaging.
  • the polymer component of the core layer is also a mixture which contains in addition to the linear polyethylene, in particular a linear low density polyethylene (LLDPE) at least one further low density polyethylene.
  • LLDPE linear low density polyethylene
  • LDPE non-linear low density polyethylene
  • mLLDPE linear low density polyethylene
  • linear polyethylene is provided as the main constituent of the polymer component of the core layer.
  • the core layer can be formed, for example, from 10 to 30 wt .-% of fillers including processing aids, 10 to 30% by weight of LDPE or mLLDPE and rest LLDPE.
  • At least one of the two outer layers or the optionally provided intermediate layer contains color particles in order to obtain an overall opaque film. It can also be exploited that the core layer is clouded by the foaming at least to a certain extent, so that then the proportion of color particles compared to a non-foamed coextrusion film may optionally be reduced.
  • the Fig. 1 shows a plastic multilayer film, which has a total thickness between 20 microns and 250 microns.
  • the plastic multilayer film has a foamed core layer 1, a first unfoamed, heat-sealable outer layer 2 and a second unfoamed outer layer 3, which has a thickness of less than 70 ⁇ m and typically between 15 ⁇ m and 40 ⁇ m.
  • the foamed core layer has cavities 4, so that the core layer 1 has a strong waviness due to the foaming. Since the two outer layers 2, 3 have a uniform or at least substantially uniform thickness, the waviness of the core layer is also present on the surfaces of the first outer layer 2 and the second outer layer 3.
  • the described waviness is not a significant limitation.
  • the second outer layer 3 is visibly arranged .
  • the surface of the second outer layer is dull. Therefore the second outer layer has a matt surface with a reflectometer value according to DIN 6753 at a measuring angle of 85 ° of less than 40, preferably less than 30 and in particular between 10 and 25.
  • the existing, relatively strong ripple is then no longer visible to a viewer as a disturbance.
  • the structure shown is preferably formed by coextrusion, wherein then during the extrusion process, the core layer 1 between the first outer layer 2 and the second outer layer 3 is included.
  • the Fig. 2 shows a plastic multilayer film in which the core layer 1 is coextruded together with the first outer layer 2 and an intermediate layer 5, wherein then on the intermediate layer, a cover sheet is laminated, which comprises as monofilm only the second outer layer.
  • the lamination can be done with adhesive 6, wherein the intermediate layer 5 or the concealed in the plastic multilayer film side of the second outer layer 3 can be provided with a print before lamination, which is then covered in the plastic multilayer film and thus optimally protected.

Landscapes

  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Laminated Bodies (AREA)

Claims (11)

  1. Film de plastique multi-couches ayant une épaisseur entre 20 µm et 250 µm comprenant une couche de coeur (1), une première couche extérieure (2) non expansée et une seconde couche extérieure (3) non expansée ayant une épaisseur inférieure à 70 µm, caractérisé en ce que la seconde couche extérieure (3) présente une surface matte avec une valeur de réflectomètre selon DIN 67530 inférieure à 40 pour un angle de mesure de 85°.
  2. Film de plastique multi-couches selon la revendication 1, caractérisé en ce que la valeur de réflectomètre selon DIN 67530 est inférieure à 30, en particulier entre 10 et 25, pour un angle de mesure de 85°.
  3. Film de plastique multi-couches selon la revendication 1 ou 2, caractérisé en ce que la couche de coeur (1) est coextrudée avec la première couche extérieure (2) et la seconde couche extérieure (3).
  4. Film de plastique multi-couches selon la revendication 1 ou 2, caractérisé en ce que la couche de coeur (1) est coextrudée avec la première couche extérieure (2) et, à l'opposé de la première couche extérieure (2), avec une couche intermédiaire (5), dans lequel le film coextrudé ainsi formé est doublé d'une couche de couverture sur la couche intermédiaire, laquelle comprend au moins la seconde couche extérieure (3).
  5. Film de plastique multi-couches selon la revendication 4, caractérisé par une empreinte placée à l'intérieur.
  6. Film de plastique multi-couches selon la revendication 4 ou 5, caractérisé en ce que la couche de couverture est orientée biaxialement.
  7. Film de plastique multi-couches selon l'une des revendications 1 à 6, caractérisé en ce que la seconde couche extérieure (3) contient du polypropylène (PP) en tant que composante principale.
  8. Film de plastique multi-couches selon l'une des revendications 1 à 6, caractérisé en ce que la seconde couche extérieure (3) contient du polyester, en particulier du polyéthylènetéréphthalate (PET) en tant que composante principale.
  9. Film de plastique multi-couches selon l'une des revendications 1 à 8, caractérisé en ce que la seconde couche extérieure (3) présente une ondulation Wa moyenne selon DIN EN ISO 4287 supérieure à 2 µm.
  10. Film de plastique multi-couches selon l'une des revendications 1 à 9, caractérisé en ce que la seconde couche extérieure (3) présente une épaisseur entre 15 µm et 40 µm.
  11. Film de plastique multi-couches selon l'une des revendications 1 à 10, caractérisé en ce que la couche de coeur (1) et la première couche extérieure (2) sont formées à base de polyéthylène (PE) en tant que composante principale.
EP14183261.8A 2014-09-02 2014-09-02 Feuille à plusieurs couches en plastique Active EP2803478B1 (fr)

Priority Applications (5)

Application Number Priority Date Filing Date Title
HUE14183261A HUE030040T2 (en) 2014-09-02 2014-09-02 Multilayer plastic film
EP14183261.8A EP2803478B1 (fr) 2014-09-02 2014-09-02 Feuille à plusieurs couches en plastique
ES14183261.8T ES2586155T3 (es) 2014-09-02 2014-09-02 Lámina multicapa de plástico
PL14183261T PL2803478T3 (pl) 2014-09-02 2014-09-02 Wielowarstwowa folia z tworzywa sztucznego
US14/809,738 US20160059514A1 (en) 2014-09-02 2015-07-27 Plastic film laminate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP14183261.8A EP2803478B1 (fr) 2014-09-02 2014-09-02 Feuille à plusieurs couches en plastique

Publications (3)

Publication Number Publication Date
EP2803478A2 EP2803478A2 (fr) 2014-11-19
EP2803478A3 EP2803478A3 (fr) 2015-04-22
EP2803478B1 true EP2803478B1 (fr) 2016-06-29

Family

ID=51453669

Family Applications (1)

Application Number Title Priority Date Filing Date
EP14183261.8A Active EP2803478B1 (fr) 2014-09-02 2014-09-02 Feuille à plusieurs couches en plastique

Country Status (5)

Country Link
US (1) US20160059514A1 (fr)
EP (1) EP2803478B1 (fr)
ES (1) ES2586155T3 (fr)
HU (1) HUE030040T2 (fr)
PL (1) PL2803478T3 (fr)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2016049049A1 (fr) 2014-09-23 2016-03-31 Dart Container Corporation Récipient isolé et procédés de fabrication et d'assemblage
DK3473674T3 (da) * 2017-10-19 2022-06-20 Abu Dhabi Polymers Co Ltd Borouge Llc Polypropylensammensætning
US20200156293A1 (en) * 2018-11-16 2020-05-21 Mucell Extrusion, Llc Anisotropic thin foamed polyethylene sheet and applications thereof
DE202019106036U1 (de) * 2019-10-30 2019-12-02 Vibracoustic Ag Lagerstrukturbauteil

Family Cites Families (72)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2038557A1 (de) 1970-08-03 1972-02-10 Lissmann Alkor Werk Verfahren zur Herstellung eines mehrschichtigen Folienschlauches
CA1145724A (fr) 1980-10-23 1983-05-03 Deane E. Galloway Sac d'emballage sous vide de viandes ou de denrees similaires
GB2110215B (en) 1981-10-31 1985-05-30 Metal Closures Venus Pack Tearable plastic film
DE3269739D1 (en) 1981-12-30 1986-04-10 Mobil Oil Corp Foam-film coextruded plastic bags
US4473665A (en) 1982-07-30 1984-09-25 Massachusetts Institute Of Technology Microcellular closed cell foams and their method of manufacture
US4533578A (en) * 1983-08-30 1985-08-06 Mobil Oil Corporation Sandwich foam coextrusion for high performance polyolefin trash bags
US4657811A (en) 1983-08-30 1987-04-14 Mobil Oil Corporation High performance three layer polyolefin film
US4522675A (en) 1983-09-14 1985-06-11 Mobil Oil Corporation Method for forming a laminated film containing different polymer layers
CA1335253C (fr) 1986-03-17 1995-04-18 Keiji Sugimoto Pellicule et emballage multicouche en plastique
US4762230A (en) 1986-10-08 1988-08-09 Warner-Lambert Company Tear oriented package
US4781294A (en) 1986-10-08 1988-11-01 Warner-Lambert Company Tear oriented package
DE3722139A1 (de) 1987-07-04 1989-01-19 Stoll Kunststoffe Gmbh & Co Kg Verfahren zur herstellung einer geschaeumten folie aus thermoplastischem kunststoff
EP0377650A1 (fr) 1987-07-29 1990-07-18 Massachusetts Institute Of Technology Procede de production de mousses microcellulaires et mousses microcellulaires en materiaux polymeres semi-cristallins
US5000992A (en) 1989-06-01 1991-03-19 The Dow Chemical Company Coextruded multilayer foamed film for plastic container closures and process for manufacture
US5215691A (en) 1990-09-05 1993-06-01 The Dow Chemical Company Method of forming a coextruded foam composite
US5158986A (en) 1991-04-05 1992-10-27 Massachusetts Institute Of Technology Microcellular thermoplastic foamed with supercritical fluid
NZ242460A (en) 1991-05-02 1995-05-26 Grace W R & Co Multilayer biaxially heat-shrinkable patch comprising two outer polymeric layers and an inner foam polymer layer
US5866053A (en) 1993-11-04 1999-02-02 Massachusetts Institute Of Technology Method for providing continuous processing of microcellular and supermicrocellular foamed materials
JP2650849B2 (ja) 1994-03-25 1997-09-10 清二 加川 易裂性積層フィルムおよびその製造方法
AU755441B2 (en) 1996-08-27 2002-12-12 Trexel, Inc. Method and apparatus for microcellular polymer extrusion
DE19646665A1 (de) 1996-11-12 1998-05-14 Linde Ag Durchflußregelung
DE19653608B4 (de) 1996-12-20 2006-03-16 Dieter Dipl.-Ing. Dengl Folien mit textilem Griff
CA2241609C (fr) * 1997-06-26 2009-08-25 Southpac Trust International, Inc. Matiere polymere ayant l'apparence d'un tissu
US6235380B1 (en) 1997-07-24 2001-05-22 Trexel, Inc. Lamination of microcellular articles
JPH1179192A (ja) 1997-09-05 1999-03-23 Takushiyoku Shoji:Kk 複合フィルム穀物袋
CN1265955C (zh) 1997-12-19 2006-07-26 特瑞塞尔公司 微孔泡沫塑料的挤塑/吹塑方法和借此制作的制品
US6231942B1 (en) 1998-01-21 2001-05-15 Trexel, Inc. Method and apparatus for microcellular polypropylene extrusion, and polypropylene articles produced thereby
TW384271B (en) 1998-04-22 2000-03-11 Lin Bo Hung Method for producing environmental friendly foamed plastic bags
EP1131387B1 (fr) 1998-06-03 2005-11-16 Trexel, Inc. Structures elastomeres thermoplastiques microcellulaires
US6114025A (en) 1998-06-15 2000-09-05 Tenneco Protective Packaging, Inc. Foam and film/foam laminates using linear low density polyethylene
US6096793A (en) 1998-12-22 2000-08-01 Sealed Air Corporation Foam comprising polyolefin blend and method for producing same
GB9912739D0 (en) 1999-06-01 1999-08-04 Borealis As Process
DE60030514T2 (de) 1999-08-12 2007-07-05 Sumitomo Chemical Co., Ltd. Mehrschichtige geschäumte Polyolefin-Folie, Verfahren und Vorrichtung zur deren Herstellung
JP2001055242A (ja) 1999-08-19 2001-02-27 Nippon Film Kk 生分解性プラスチック袋
US6403663B1 (en) 1999-09-20 2002-06-11 North Carolina State University Method of making foamed materials using surfactants and carbon dioxide
JP2001130586A (ja) 1999-11-09 2001-05-15 Fuji Seal Inc 口栓付きパウチ
DE19958663A1 (de) 1999-12-06 2001-06-21 Stankiewicz Gmbh Leichte Schallisolation mit partieller Trittfestigkeit
WO2001089794A1 (fr) 2000-05-25 2001-11-29 Trexel, Inc. Traitement de mousse polymere a l'aide de faibles taux d'agent d'expansion
KR100745227B1 (ko) 2000-05-26 2007-08-01 다우 글로벌 테크놀로지스 인크. 폴리에틸렌 풍부/폴리프로필렌 블렌드 및 그의 용도
WO2002006386A2 (fr) 2000-07-13 2002-01-24 Marrelli John C Films de thermoplastique expanse
US6616434B1 (en) 2000-08-10 2003-09-09 Trexel, Inc. Blowing agent metering system
JP4478319B2 (ja) 2000-11-17 2010-06-09 大日本印刷株式会社 易開封性包装袋
US20040038018A1 (en) 2002-08-22 2004-02-26 Trexel, Inc. Thermoplastic elastomeric foam materials and methods of forming the same
JP2004091024A (ja) 2002-09-03 2004-03-25 Toppan Printing Co Ltd 包装体
US7144532B2 (en) 2002-10-28 2006-12-05 Trexel, Inc. Blowing agent introduction systems and methods
US6913389B2 (en) 2002-12-20 2005-07-05 Sealed Air Corporation (Us) Metallic laminated gusseted insulated bag
WO2005007729A1 (fr) 2003-07-07 2005-01-27 Dow Global Technologies Inc. Feuilles minces de polyethylene expanse
JP3823967B2 (ja) 2003-11-18 2006-09-20 東洋製罐株式会社 易引裂き性包装袋
KR20040007381A (ko) 2003-12-29 2004-01-24 이정민 발포수지층을 이용한 포장용 필름 및 그 필름으로 제작된스파우트 파우치 용기
KR20040005806A (ko) 2003-12-29 2004-01-16 이정민 발포수지층을 이용한 포장용 필름 및 그 필름으로 제작된스파우트 파우치 용기
DE202005002615U1 (de) 2004-02-27 2005-05-19 Rkw Ag Rheinische Kunststoffwerke Dünnfolien mit niedriger Dichte
US7435462B2 (en) * 2004-05-28 2008-10-14 Arkema France Thermoplastic article with a printable matte surface
US20060003121A1 (en) 2004-06-30 2006-01-05 Scheller Joseph A Abrasive article packaging and method of making same
JP4904672B2 (ja) 2004-07-20 2012-03-28 東洋紡績株式会社 ヒートシール性ポリオレフィン系発泡フィルム
EP1857501A4 (fr) 2005-01-31 2009-02-18 Jsr Corp Procede de formation d'une mousse moulee et mousse moulee
DE102005020794A1 (de) 2005-05-04 2006-11-09 Coperion Werner & Pfleiderer Gmbh & Co. Kg Anlage zur Erzeugung einer Schaumkunststoff-Folie
FR2886938B1 (fr) 2005-06-10 2008-04-18 Armines Ass Loi De 1901 Procede d'extrusion permettant de fabriquer des dispersions solides de principes actifs pharmaceutiques dans une matrice polymere
JP2007045047A (ja) 2005-08-11 2007-02-22 Toyobo Co Ltd ヒートシール性ポリオレフィン系発泡フイルム
JP2007045046A (ja) 2005-08-11 2007-02-22 Toyobo Co Ltd 高隠蔽性ヒートシール性ポリオレフィン系発泡フイルム
ITPD20060022A1 (it) 2006-01-24 2007-07-25 Alcan Packaging Italia Srl Film laminato multistrato
JP2007230637A (ja) 2006-03-03 2007-09-13 Toppan Printing Co Ltd 耐ピンホール性を付与した包装フィルム及び包装袋
US20100273377A1 (en) * 2006-06-29 2010-10-28 Files John C High Strength Packages and Packaging Materials
US7993739B2 (en) 2006-07-14 2011-08-09 Dow Global Technologies Llc Anisotropic foam-film composite structures
WO2008100501A2 (fr) 2007-02-13 2008-08-21 Dow Global Technologies Inc. Mousse de polyoléfine souple au toucher
WO2009155326A1 (fr) 2008-06-20 2009-12-23 The Procter & Gamble Company Emballage de film mousse
DE102009041341A1 (de) 2009-05-19 2010-11-25 Huhtamaki Forchheim Zweigniederlassung Der Huhtamaki Deutschland Gmbh & Co. Kg Leicht zu öffnende Verpackung
DE102011000399A1 (de) 2011-01-28 2012-08-02 Benecke-Kaliko Ag Verfahren zur Herstellung einer mehrschichtigen Kunststofffolie
DE102011051193A1 (de) * 2011-06-20 2012-12-20 Nordenia Technologies Gmbh Seitenfaltenbeutel zur Verpackung von stückigem und körnigem Schüttgut
JP5840471B2 (ja) 2011-11-28 2016-01-06 株式会社細川洋行 発泡層を有する易剥離性フィルム
KR101316705B1 (ko) 2012-03-02 2013-10-18 주식회사 알앤에프케미칼 디스플레이 제품 포장용 폼 합지 폴리에틸렌 필름
JP5509370B1 (ja) 2012-05-28 2014-06-04 日東電工株式会社 樹脂発泡体、発泡部材、発泡部材積層体及び電気又は電子機器類
DE102012108705B4 (de) * 2012-09-17 2020-01-09 Mondi Ag Kunststofffolie

Also Published As

Publication number Publication date
ES2586155T3 (es) 2016-10-11
PL2803478T3 (pl) 2017-02-28
HUE030040T2 (en) 2017-04-28
EP2803478A3 (fr) 2015-04-22
EP2803478A2 (fr) 2014-11-19
US20160059514A1 (en) 2016-03-03

Similar Documents

Publication Publication Date Title
DE602005000810T2 (de) Verfahren und vorrichtung zur herstellung einer sandwich-folie
DE60030514T2 (de) Mehrschichtige geschäumte Polyolefin-Folie, Verfahren und Vorrichtung zur deren Herstellung
DE69921506T2 (de) Mehrschichtige struktur zur verpackung und daraus hergestellte verpackungsbehälter, sowie verfahren zur herstellung dieser struktur
EP2815879A2 (fr) Feuille de coextrusion en polyéthylène
DE69307742T2 (de) Kunststoff-Mehrschichtfolie und Verfahren zu ihrer Herstellung
EP1885558B2 (fr) Feuille-barriere multicouche coextrudee comportant au moins une couche de feuille a base de copolymere ethylene-alcool vinylique (evoh), son procede de production, et son utilisation
DE102012108705B4 (de) Kunststofffolie
DE102005020913B3 (de) Hochfeste Barrierefolie für Verpackungszwecke auf Polypropylenbasis, Verfahren zu ihrer Herstellung und ihre Verwendung
EP0809571B1 (fr) Procede de fabrication de materiaux d'emballage constitues d'une couche de polyolefine moussee
EP0616885B1 (fr) Feuille en polypropylène étirée biaxialement et à surface mate, et son procédé de fabrication
EP2803478B1 (fr) Feuille à plusieurs couches en plastique
DE3736102A1 (de) Klebeband, bei dem ein klebstoff auf einen traeger aus einem stoffmaterial und einer kunststoffschicht geschichtet ist
EP3265290B1 (fr) Procede de fabrication d'une bande de film multicouches et bande de film multicouches
EP2258545B1 (fr) Emballage pouvant s'ouvrir facilement
EP3600889B1 (fr) Laminé d'emballage recyclable ayant une résistance à la chaleur améliorée pendant le scellage
EP2471652A1 (fr) Matière en couche élastomère et son procédé de fabrication
EP2813441A1 (fr) Emballage déchirable pour feuilles et utilisation d'un film coextrudé flexible à au moins trois couches pour la fabrication d'un emballage déchirable pour feuilles
DE3239167A1 (de) Coextrudierte thermoplastische verbundfolie und verfahren zu ihrer herstellung
DE19544858C2 (de) Verfahren zum Herstellen einer thermogeformten Verpackung
DE3752076T2 (de) Anbringen von Etiketten auf Plastikbehältern
EP2094465A1 (fr) Procédé de production d'un laminé multicouche, et laminé multicouche ainsi obtenu
EP2024156A1 (fr) Procédé de fabrication d'une feuille de plastique extrudée et utilisation de la feuille de plastique
WO2008037447A1 (fr) Sachet à fond plat constitué d'une feuille multicouche
DE102005029156B4 (de) Laminat für Tuben- und Behälterkonstruktionen
DE3787415T2 (de) Wärmeschrumpfbare Folie.

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20140902

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

RIC1 Information provided on ipc code assigned before grant

Ipc: B32B 27/36 20060101ALI20150316BHEP

Ipc: B32B 27/32 20060101ALI20150316BHEP

Ipc: B32B 5/18 20060101AFI20150316BHEP

Ipc: B32B 27/06 20060101ALI20150316BHEP

R17P Request for examination filed (corrected)

Effective date: 20150410

RBV Designated contracting states (corrected)

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

INTG Intention to grant announced

Effective date: 20160405

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: AT

Ref legal event code: REF

Ref document number: 808754

Country of ref document: AT

Kind code of ref document: T

Effective date: 20160715

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502014001008

Country of ref document: DE

REG Reference to a national code

Ref country code: SE

Ref legal event code: TRGR

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: KELLER AND PARTNER PATENTANWAELTE AG, CH

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 3

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2586155

Country of ref document: ES

Kind code of ref document: T3

Effective date: 20161011

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: NO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160929

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20160629

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: HR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160930

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: RS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161029

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20161031

Ref country code: SM

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20160930

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502014001008

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

REG Reference to a national code

Ref country code: HU

Ref legal event code: AG4A

Ref document number: E030040

Country of ref document: HU

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

26N No opposition filed

Effective date: 20170330

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

REG Reference to a national code

Ref country code: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20160902

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20160902

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160929

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 4

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20160930

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

Ref country code: MT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 5

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20160629

REG Reference to a national code

Ref country code: CH

Ref legal event code: PFA

Owner name: MONDI CONSUMER PACKAGING TECHNOLOGIES GMBH, DE

Free format text: FORMER OWNER: MONDI CONSUMER PACKAGING TECHNOLOGIES GMBH, DE

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 502014001008

Country of ref document: DE

Owner name: MONDI AG, AT

Free format text: FORMER OWNER: MONDI CONSUMER PACKAGING TECHNOLOGIES GMBH, 48599 GRONAU, DE

REG Reference to a national code

Ref country code: HU

Ref legal event code: GB9C

Owner name: MONDI AG, AT

Free format text: FORMER OWNER(S): MONDI CONSUMER PACKAGING TECHNOLOGIES GMBH, DE

Ref country code: HU

Ref legal event code: FH1C

Free format text: FORMER REPRESENTATIVE(S): DANUBIA SZABADALMI ES JOGI IRODA KFT., HU

Representative=s name: DANUBIA SZABADALMI ES JOGI IRODA KFT., HU

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

Free format text: REGISTERED BETWEEN 20220526 AND 20220601

REG Reference to a national code

Ref country code: ES

Ref legal event code: PC2A

Owner name: MONDI AG

Effective date: 20220628

REG Reference to a national code

Ref country code: AT

Ref legal event code: PC

Ref document number: 808754

Country of ref document: AT

Kind code of ref document: T

Owner name: MONDI GRONAU GMBH, DE

Effective date: 20220607

P01 Opt-out of the competence of the unified patent court (upc) registered

Effective date: 20230504

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: TR

Payment date: 20230901

Year of fee payment: 10

Ref country code: GB

Payment date: 20230920

Year of fee payment: 10

Ref country code: AT

Payment date: 20230921

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20230920

Year of fee payment: 10

Ref country code: PL

Payment date: 20230825

Year of fee payment: 10

Ref country code: HU

Payment date: 20230922

Year of fee payment: 10

Ref country code: FR

Payment date: 20230928

Year of fee payment: 10

Ref country code: DE

Payment date: 20230830

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20231124

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20230927

Year of fee payment: 10

Ref country code: CH

Payment date: 20231001

Year of fee payment: 10